CN207031347U - A kind of high-temperature retorting system - Google Patents
A kind of high-temperature retorting system Download PDFInfo
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- CN207031347U CN207031347U CN201720171672.8U CN201720171672U CN207031347U CN 207031347 U CN207031347 U CN 207031347U CN 201720171672 U CN201720171672 U CN 201720171672U CN 207031347 U CN207031347 U CN 207031347U
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Abstract
It the utility model is related to a kind of high-temperature retorting system, including main stove, horizontal revolving retort is equipped with main stove, horizontal revolving retort both ends are driven by gear by power motor respectively to rotate, horizontal revolving retort exit is connected with outlet integrated device of slagging tap, outlet integrated device of slagging tap is connected by blast pipe with liquefied gas condensing unit, and liquefied gas condensing unit end is connected with liquefied gas filter recycle device, and main furnace roof portion is connected with Multi-stage dust removing device.The beneficial effects of the utility model are：Material can be made to carry out heating destructive distillation in motion process, and it can be heated liquefied gas caused by destructive distillation, accumulation can be prevented to cause production not continue caused by destructive distillation is sticky, the liquefied gas for obtaining destructive distillation while slagging tap while discharged, flue gas has met discharge standard；Slag discharge efficiency is high, and floor space is small, easy access, energy-conserving and environment-protective, and integrated degree is high, and liquefied gas condensation effect is good.
Description
（One）Technical field
The invention belongs to chemical production technical field, more particularly to a kind of high-temperature retorting system.
（Two）Background technology
China is second-biggest-in-the-world energy resource consumption state, consumes about 600,000,000 tons of crude oil every year, and the ratio of crude oil import amount exceedes
55%, internationally recognized 50% warning line is had passed past, and the ratio of imported crude oil will also continue to increase, due to international situation
Complicated and changeable, the situation of long-term heavy dependence external import crude oil be will be unable to be guaranteed, and following energy supply is not known
Property will restrict the continual and steady sound development of China's economy, and crude oil has turned into the powerful mean that U.S. etc. manipulates world's situation,
Serious threat will certainly be caused to China.
The oil shale ore reserves very abundant in China, proven reserve position is at the forefront in the world, is carried from oil shale ore
Take the prospect of shale oil very wide, have to the interdependency and guarantee China's economic security for reducing China's external oil important
Strategic importance.
In addition, house refuse cannot be handled effectively, slowly accumulation over time, environment can be not only influenceed, and
Cause and greatly waste, effectively do not applied and handled.
At present, the technique that shale oil is extracted from oil shale ore is carried out using low pressure shaft furnace, is had the disadvantage that：
Heat it is uneven, and can not persistently to oil shale ore carry out destructive distillation processing, it is necessary to disconnect the stove of a stove one carry out；Caused by destructive distillation
Waste gas could not be applied effectively, not meet the general requirement of national energy-saving environmental protection；For caused by the high-temperature heating destructive distillation of main stove
Flue gas has been directly discharged in air, and environment has been damaged because it has serious contaminative, there is presently no to this flue gas compared with
Good treating method；Without Action of Gravity Field, the difficulty that the slag charge after destructive distillation comes out from main stove just increases, and is easily deposited in master
Stove fire door, it is impossible to quickly smoothly leave main stove, the destructive distillation to main stove causes trouble, and What is more can damage main stove etc. and match somebody with somebody
Part；It is separated to slag tap with outlet, not only increases the difficulty of processing of equipment, and floor space is big, and operation maintenance is also number
It is tired；The liquefaction air tightness that high-temperature retorting goes out is uneven, is not condensed respectively, and condensation efficiency is very low；In addition, condensation is situated between
Matter do not obtain it is good recycle, even if recycle, cooling medium temperature is quickly lowered yet, condensation effect
Fruit is bad.
（Three）The content of the invention
The present invention is in order to make up the deficiencies in the prior art, there is provided a kind of homogeneous heating, efficiency high, can continuous production, section
Can environmental protection, the high-temperature retorting system that safe and reliable, floor space is small, easy access, integrated degree are high.
The present invention is achieved through the following technical solutions：
A kind of high-temperature retorting system, including main stove, it is characterized in that：Horizontal revolving retort is equipped with the main stove, is crouched
Formula rotary dry distillation kettle both ends are driven by gear by power motor respectively to be rotated, and horizontal revolving retort exit is connected with out
Slag outlet integrated device, outlet integrated device of slagging tap are connected by blast pipe with liquefied gas condensing unit, liquefied gas condensation dress
Set terminal is connected with liquefied gas filter recycle device, and main furnace roof portion is connected with Multi-stage dust removing device.
The power motor of the horizontal revolving retort porch is fixed on bottom plate, and bottom plate is placed in fixed seat, bottom plate
Some first springs are provided between fixed seat.
Copy plate is provided with the horizontal revolving retort outlet, copy plate is fixedly installed in horizontal revolving retort front end
End cap on.
The outlet integrated device of slagging tap includes the residue outlet stretched into horizontal revolving retort, is provided with and slags tap in residue outlet
Spiral, residue outlet outsourcing are provided with outer barrel, and outer barrel passes through gas bag, and pipe end of slagging tap bottom is connected with scum pipe, is provided with scum pipe
Deslagging spiral.
The gas bag is installed on base, and base is made up of upper plate and lower shoe, is installed between upper plate and lower shoe
There are some second springs, spiral of slagging tap is connected with motor of slagging tap, and deslagging spiral is connected with deslagging motor.
The liquefied gas condensing unit includes the liquefied gas air inlet pipe being connected with blast pipe, and liquefied gas air inlet pipe is with separating
Cylinder is connected, and cylinder bottom is connected with heavy oil condensing tower, is connected at the top of cylinder with light oil condensing tower, heavy oil condensing tower
Be respectively equipped with condensation matrix in light oil condensing tower, condensation baseline top is connected with oral siphon, condensation base bottom and water outlet
Pipe is connected, and oral siphon is connected with the side bottom of condensation water tank one, and outlet pipe condenses with being connected at the top of condensation water tank opposite side
Some baffle plates are provided with water tank.
The liquefied gas filter recycle device includes the air inlet pipe being connected with liquefied gas condensing unit end, air inlet pipe
Primary holding vessel is connected, primary holding vessel is connected with some filtering tanks in turn, and end filtration tank is connected with filtering total tank, filters
Total tank is connected with net gas tank, and net gas tank is connected with the escape pipe for the supply burning of main stove, is done if being connected with escape pipe
Gas branch pipe, going out gas branch pipe are stretched into main stove.
The Multi-stage dust removing device includes the smoke inlet pipe being connected with main stove, and smoke inlet pipe removes dirt cup phase with some levels
Connection, remove per two-stage and be connected by smoke conveying duct between dirt cup, if except being laid with dried layer successively from top to bottom in dirt cup
Screen pack, except some showers are connected with the top of dirt cup, shower is connected by water inlet pipe with dust-proof water tank, except dirt cup bottom
Drainpipe is connected with, drainpipe is connected by main sewer with dust-proof water tank.
It is described except dirt cup is three-level, smoke inlet pipe is with the first order except dirt cup bottom is connected, and the first order is except at the top of dirt cup
With the second level except being connected at the top of dirt cup, dirt cup bottom is removed with the third level except dirt cup bottom is connected in the second level, third level dedusting
Cylinder top is provided with smoke discharge tube, and screen pack is 50 layers.
The horizontal revolving retort porch is connected with into charging basket.
The beneficial effects of the invention are as follows：Material can be made to carry out heating destructive distillation in motion process, and can be used caused by destructive distillation
Liquefied gas is heated, and can prevent that accumulation causes production not continue caused by destructive distillation is sticky, by destructive distillation while slagging tap
Obtained liquefied gas while discharge, flue gas is multistage except under the filtering of the spray and screen pack of dirt cup, having met discharge standard；Go out
Slag efficiency high, floor space are small, easy access, energy-conserving and environment-protective, integrated degree is high, liquefied gas condensation efficiency is high, and condense
Effect is good, provides and significantly facilitates for the high-temperature retorting of oil shale and house refuse etc..
（Four）Brief description of the drawings
The present invention is further illustrated below in conjunction with the accompanying drawings.
Accompanying drawing 1 is the structural representation of the present invention；
Accompanying drawing 2 is power motor mounting structure schematic diagram of the invention；
Accompanying drawing 3 is copy plate mounting structure schematic diagram of the invention；
Accompanying drawing 4 is outlet integrated device structural representation of slagging tap of the invention；
Accompanying drawing 5 is condensation basal body structure schematic diagram of the invention；
In figure, 1 main stove, 2 horizontal revolving retorts, 3 gears, 4 power motors, 5 slag tap outlet integrated device, 6 blast pipes,
7 liquefied gas condensing units, 8 liquefied gas filter recycle devices, 9 Multi-stage dust removing devices, 10 bottom plates, 11 fixed seats, 12 first
Spring, 13 copy plates, 14 end caps, 51 residue outlets, 52 slag tap spiral, 53 outer barrels, 54 gas bags, 55 scum pipes, 56 deslagging spirals,
57 bases, 58 upper plates, 59 lower shoes, 510 second springs, 511 slag tap motor, 512 deslagging motors, 71 liquefied gas air inlet pipe,
72 cylinders, 73 heavy oil condensing towers, 74 light oil condensing towers, 75 condensation matrixes, 76 oral siphons, 77 outlet pipes, 78 condensation water tanks,
79 baffle plates, 81 air inlet pipe, 82 primary holding vessels, 83 filtering tanks, the 84 total tanks of filtering, 85 net gas tanks, 86 escape pipes, 87 outlet branch
Pipe, 91 smoke inlet pipes, 92 remove dirt cup, 93 smoke conveying ducts, 94 screen packs, 95 showers, 96 water inlet pipes, 97 water in dust removal
Case, 98 drainpipes, 99 main sewers, 910 first order remove dirt cup, and dirt cup is removed in 911 second level, and 912 third level remove dirt cup, 913 cigarettes
Gas discharge pipe, 15 enter charging basket.
（Five）Embodiment
Accompanying drawing is a kind of specific embodiment of the invention.The embodiment includes main stove 1, and horizontal revolving is equipped with main stove 1
Retort 2, the both ends of horizontal revolving retort 2 drive rotation by gear 3 by power motor 4 respectively, and horizontal revolving retort 2 goes out
Outlet integrated device 5 of slagging tap is connected with mouthful, outlet integrated device 5 of slagging tap passes through blast pipe 6 and the phase of liquefied gas condensing unit 7
Connection, the end of liquefied gas condensing unit 7 are connected with liquefied gas filter recycle device 8, and the main top of stove 1 is connected with multistage dedusting
Device 9.The power motor 4 of the porch of horizontal revolving retort 2 is fixed on bottom plate 10, and bottom plate 10 is placed in fixed seat 11, bottom
Some first springs 12 are provided between plate 10 and fixed seat 11.Horizontal revolving retort 2 is provided with copy plate 13, copy plate in exporting
13 are fixedly installed on the end cap 14 of the front end of horizontal revolving retort 2.Outlet integrated device 5 of slagging tap is done including stretching into horizontal revolving
The residue outlet 51 in kettle 2 is evaporated, is provided with spiral 52 of slagging tap in residue outlet 51, the outsourcing of residue outlet 51 is provided with outer barrel 53, and outer barrel 53 passes through
Gas bag 54, the end bottom of residue outlet 51 are connected with scum pipe 55, deslagging spiral 56 are provided with scum pipe 55.Gas bag 54 is installed on bottom
On seat 57, base 57 is made up of upper plate 58 and lower shoe 59, and some second bullets are provided between upper plate 58 and lower shoe 59
Spring 510, spiral 52 of slagging tap are connected with motor 511 of slagging tap, and deslagging spiral 56 is connected with deslagging motor 512.Liquefied gas condenses
Device 7 includes the liquefied gas air inlet pipe 71 being connected with blast pipe 6, and liquefied gas air inlet pipe 71 is connected with cylinder 72, separates
72 bottoms of cylinder are connected with heavy oil condensing tower 73, and the top of cylinder 72 is connected with light oil condensing tower 74, the He of heavy oil condensing tower 73
Condensation matrix 75 is respectively equipped with light oil condensing tower 74, the top of condensation matrix 75 is connected with oral siphon 76, condensation matrix 75 bottom
Portion is connected with outlet pipe 77, and oral siphon 76 is connected with the side bottom of condensation water tank 78 1, and outlet pipe 77 and condensation water tank 78 are another
One side roof part is connected, and some baffle plates 79 are provided with condensation water tank 78.Liquefied gas filter recycle device 8 includes and liquefied gas
The air inlet pipe 81 of the end of condensing unit 7 connection, air inlet pipe 81 connects primary holding vessel 82, if primary holding vessel 82 is connected with turn
Dry filtering tank 83, end filtration tank 83 are connected with filtering total tank 84, filter total tank 84 and be connected with net gas tank 85, net gas tank 85
The escape pipe 86 for the supply burning of main stove 1 is connected with, is connected with some going out gas branch pipe 87 on escape pipe 86, going out gas branch pipe 87 is stretched
Become owner of in stove 1.Multi-stage dust removing device 9 includes the smoke inlet pipe 91 being connected with main stove 1, smoke inlet pipe 91 and some grades of dedustings
Cylinder 92 is connected, and removes per two-stage and is connected by smoke conveying duct 93 between dirt cup 92, except in dirt cup 92 from top to bottom successively
If being laid with dried layer screen pack 94, except the top of dirt cup 92 is connected with some showers 95, shower 95 is by water inlet pipe 96 with removing
Dirt water tank 97 is connected, and except the bottom of dirt cup 92 is connected with drainpipe 98, drainpipe 98 passes through main sewer 99 and dust-proof water tank 97
It is connected.Except dirt cup 92 is three-level, for smoke inlet pipe 91 with the first order except the bottom of dirt cup 910 is connected, the first order removes dirt cup 910
Top is with the second level except the top of dirt cup 911 is connected, and the second level is except the bottom of dirt cup 911 with the third level except the bottom of dirt cup 912 is connected
Connect, the third level is provided with smoke discharge tube 913 except the top of dirt cup 912, and screen pack 94 is 50 layers.The porch of horizontal revolving retort 2
It is connected with into charging basket 15.
Using a kind of high-temperature retorting system of the present invention, the materials such as oil shale or house refuse are placed in charging basket 15,
Power motor 4 is rotated by reductor band moving gear 3, so as to drive horizontal revolving retort 2 to rotate, in horizontal revolving retort
While 2 rotation, the spiral push pedal in horizontal revolving retort 2 drives material slowly to push ahead, at the same time, in main stove 1
Gas burns to heat to horizontal revolving retort 2 carries out high-temperature retorting to it to material.Slag charge after high-temperature retorting and
Caused liquefied gas is discharged by outlet integrated device 5 of slagging tap, and the liquefied gas of discharge enters liquefied gas condensing unit 7, after condensation
Liquefied gas be admitted to liquefied gas filter recycle device 8 and turn into net gas, net gas stores rear portion and can sent again
Become owner of to be burnt in stove 1 and high-temperature heating destructive distillation is carried out to material, flue gas caused by high-temperature heating destructive distillation is filled by multistage dedusting
Arranged after putting 9 purified treatments as the flue gas for meeting discharge standard to air.
, can be to power motor 4 due to the effect of the first spring 12 when gear 3 is driven by power motor and has back lash
Quick regulation is carried out, prevents from breaking broken teeth wheel 3, avoids the generation of production accident.
Material in horizontal revolving retort 2 slowly moves forward when carrying out high-temperature retorting, is moved to horizontal time
It is slag charge to turn during 2 front end of retort, and because horizontal revolving retort 2 is relatively large in diameter, and the diameter of residue outlet 51 is smaller, and slag charge is very
It is difficult to be fast and effeciently advanced into residue outlet 51 certainly, however, copy plate 13 turns together with horizontal revolving retort 2 and end cap 14
Dynamic, the copy plate 13 of rotation can endlessly be taken up slag charge, with its rotation, you can slag charge is copied into residue outlet 51,
Spiral 52 of slagging tap drives slag charge to proceed to scum pipe 55 and discharged.
The slag come out from horizontal revolving retort 2 enters residue outlet 51, and motor 511 of slagging tap drives spiral 52 of slagging tap to rotate will
Slag, which is taken out of, falls into scum pipe 55, and deslagging motor 512 drives deslagging spiral 56 to rotate and discharges slag.At the same time, from horizontal revolving
The liquefied gas that retort 2 comes out enters between residue outlet 51 and outer barrel 53 hence into gas bag 54, is then discharged by blast pipe 6
To carry out filtering utilization.Because the end of horizontal revolving retort 2 being connected with residue outlet 51 and slag output end are rotations, easily produce
Raw gap, second spring 510 can move up and down gas bag 54 to be adjusted, situations such as to prevent fracture.
The liquefied gas come out from outlet integrated device 5 of slagging tap enters cylinder 72 by liquefied gas air inlet pipe 71, is separating
In cylinder 72, the big liquefied gas of density can sink ascends into light oil condensing tower into heavy oil condensing tower 73, the small liquefied gas of density
74, so the different liquefied gas of density is separately condensed, the condensation prevented is not in place, and some has condensed to
Position also continue condensation the problem of, not only condensation effect is good, and has saved cost.Respectively enter heavy oil condensing tower 73 and light oil
The liquefied gas of condensing tower 74 is descending, passes through during descending and is handed over the cooling medium heat to be circulated in condensation matrix 75 in condenser pipe
Change and condense out.Cooling medium is extracted by oral siphon 76 from condensation water tank 78, and cooling medium is descending from the top of condensation matrix 75
To during bottom condensation water tank 78 is discharged into from outlet pipe 77.The cooling medium discharged from outlet pipe 77 flows into baffle plate 79 and condensation water tank
In the spaces of 78 compositions, just outflow when cooling medium liquid level is concordant with first piece of baffle plate 79, second piece of baffle plate 79 of inflow, the
In the space that one piece of baffle plate 79 forms with condensation water tank 78, between being left due to second piece of bottom of baffle plate 79 and the bottom of condensation water tank 78
Gap, cooling medium continue to move ahead, and reach in the space that second piece of baffle plate 79, condensation water tank 78 and the 3rd piece of baffle plate 79 form, cold
Solidifying medium will not move ahead, and be blocked by the 3rd piece of baffle plate 79, until when liquid level is raised to concordant with the 3rd piece of top of baffle plate 79 again
It may proceed to flow forward, so repeat, cooling medium is rolled up and down forward, make the cooling medium after heat exchange quick
Cooling is got off, and carries out heat exchange in order to go successively to condensing tower so that more preferably, condensation efficiency is higher for condensation effect.
The liquefied gas come out from liquefied gas condensing unit 7 enters primary holding vessel 82 by air inlet pipe 81 respectively, in primary
After the interior buffering of holding vessel 82 and primary filter, liquefied gas enters filtering tank 83, after the filtering of double-filtration tank 83, every group of liquefaction
Gas respectively enters the total tank 84 of filtering, and liquefied gas turns into net gas after filtering the filtering of total tank 84, and net gas enters into net gas tank 85
The final storage of row, at the same the net gas in net gas tank 85 discharged by escape pipe 86 after evenly distributing pair by going out gas branch pipe 87
Main stove 1 carries out homogenous combustion heating.
Enter smoke inlet pipe 91 from the flue gas of main stove 1 discharge, in the presence of centrifugal blower, flue gas quickly enters first
Level remove the bottom of dirt cup 910, and subsequent flue gas is up to up to the first order except the top of dirt cup 910, by smoke conveying duct 93 into the
The top of two-stage dust removal cylinder 911, subsequent flue gas go downwards to up to the second level and remove the bottom of dirt cup 911, entered by smoke conveying duct 93
The third level removes the bottom of dirt cup 912, finally in the third level except the top of dirt cup 912 by the row of smoke discharge tube 913 to air.In this way,
Flue gas is at every grade except dirt cup 92 is through by have passed through the filtering of 50 layers of screen pack 94, and remove in dirt cup 92 each
The spray process of shower 95 is have passed through, the pollutants such as the particulate matter in flue gas are all eliminated, have complied with the mark of discharge
It is accurate.The water that shower 95 sprays is fallen on except the bottom of dirt cup 92, is pooled to main sewer 99 by drainpipe 98, is eventually passed back to dedusting
Water tank 97, reusable edible.
Claims (10)
1. a kind of high-temperature retorting system, including main stove（1）, it is characterized in that：The main stove（1）Inside it is equipped with horizontal revolving retort
（2）, horizontal revolving retort（2）Both ends pass through gear respectively（3）By power motor（4）Drive rotation, horizontal revolving retort
（2）Exit is connected with outlet integrated device of slagging tap（5）, outlet integrated device of slagging tap（5）Pass through blast pipe（6）With liquefied gas
Condensing unit（7）It is connected, liquefied gas condensing unit（7）End is connected with liquefied gas filter recycle device（8）, main stove
（1）Top is connected with Multi-stage dust removing device（9）.
2. a kind of high-temperature retorting system according to claim 1, it is characterized in that：The horizontal revolving retort（2）Entrance
The power motor at place（4）It is fixed on bottom plate（10）On, bottom plate（10）It is placed in fixed seat（11）On, bottom plate（10）With fixed seat（11）
Between be provided with some first springs（12）.
3. a kind of high-temperature retorting system according to claim 1, it is characterized in that：The horizontal revolving retort（2）Outlet
It is interior to be provided with copy plate（13）, copy plate（13）It is fixedly installed in horizontal revolving retort（2）The end cap of front end（14）On.
4. a kind of high-temperature retorting system according to claim 1, it is characterized in that：The outlet integrated device of slagging tap（5）Bag
Include and stretch into horizontal revolving retort（2）Interior residue outlet（51）, residue outlet（51）It is interior to be provided with spiral of slagging tap（52）, residue outlet（51）
Outsourcing is provided with outer barrel（53）, outer barrel（53）Through gas bag（54）, residue outlet（51）End bottom is connected with scum pipe（55）, deslagging
Pipe（55）It is interior to be provided with deslagging spiral（56）.
5. a kind of high-temperature retorting system according to claim 4, it is characterized in that：The gas bag（54）It is installed on base（57）
On, base（57）By upper plate（58）And lower shoe（59）Form, upper plate（58）With lower shoe（59）Between be provided with it is some
Second spring（510）, spiral of slagging tap（52）With motor of slagging tap（511）It is connected, deslagging spiral（56）With deslagging motor（512）Phase
Connection.
6. a kind of high-temperature retorting system according to claim 1, it is characterized in that：The liquefied gas condensing unit（7）Including
With blast pipe（6）The liquefied gas air inlet pipe being connected（71）, liquefied gas air inlet pipe（71）With cylinder（72）It is connected, cylinder
（72）Bottom and heavy oil condensing tower（73）It is connected, cylinder（72）Top and light oil condensing tower（74）It is connected, heavy oil condensation
Tower（73）With light oil condensing tower（74）Inside it is respectively equipped with condensation matrix（75）, condense matrix（75）Top and oral siphon（76）It is connected
Connect, condense matrix（75）Bottom and outlet pipe（77）It is connected, oral siphon（76）With condensation water tank（78）One side bottom is connected,
Outlet pipe（77）With condensation water tank（78）It is connected at the top of opposite side, condensation water tank（78）It is interior to be provided with some baffle plates（79）.
7. a kind of high-temperature retorting system according to claim 1, it is characterized in that：The liquefied gas filter recycle device
（8）Including with liquefied gas condensing unit（7）The air inlet pipe of end connection（81）, air inlet pipe（81）Connect primary holding vessel（82）,
Primary holding vessel（82）It is connected with some filtering tanks in turn（83）, end filtration tank（83）With filtering total tank（84）It is connected, mistake
Filter total tank（84）With net gas tank（85）It is connected, net gas tank（85）It is connected with and is used for main stove（1）Supply the escape pipe of burning（86）,
Escape pipe（86）On be connected with some going out gas branch pipe（87）, going out gas branch pipe（87）Stretch into main stove（1）It is interior.
8. a kind of high-temperature retorting system according to claim 1, it is characterized in that：The Multi-stage dust removing device（9）Including with
Main stove（1）The smoke inlet pipe of connection（91）, smoke inlet pipe（91）Dirt cup is removed with some levels（92）It is connected, per two-stage dedusting
Cylinder（92）Between pass through smoke conveying duct（93）It is connected, except dirt cup（92）If inside it is laid with dried layer filtering successively from top to bottom
Net（94）, except dirt cup（92）Top is connected with some showers（95）, shower（95）Pass through water inlet pipe（96）With dust-proof water tank
（97）It is connected, except dirt cup（92）Bottom is connected with drainpipe（98）, drainpipe（98）Pass through main sewer（99）With water in dust removal
Case（97）It is connected.
9. a kind of high-temperature retorting system according to claim 8, it is characterized in that：It is described to remove dirt cup（92）For three-level, flue gas
Air inlet pipe（91）Dirt cup is removed with the first order（910）Bottom is connected, and the first order removes dirt cup（910）Dirt cup is removed with the second level in top
（911）Top is connected, and dirt cup is removed in the second level（911）Dirt cup is removed with the third level in bottom（912）Bottom is connected, third level dedusting
Cylinder（912）Top is provided with smoke discharge tube（913）, screen pack（94）For 50 layers.
10. a kind of high-temperature retorting system according to claim 1, it is characterized in that：The horizontal revolving retort（2）Entrance
Place is connected with into charging basket（15）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720171672.8U CN207031347U (en) | 2017-02-24 | 2017-02-24 | A kind of high-temperature retorting system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720171672.8U CN207031347U (en) | 2017-02-24 | 2017-02-24 | A kind of high-temperature retorting system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207031347U true CN207031347U (en) | 2018-02-23 |
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ID=61471588
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201720171672.8U Active CN207031347U (en) | 2017-02-24 | 2017-02-24 | A kind of high-temperature retorting system |
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| Country | Link |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106635082A (en) * | 2017-02-24 | 2017-05-10 | 山东腾鲁环保设备有限公司 | High-temperature dry distillation system |
| CN108485815A (en) * | 2018-05-29 | 2018-09-04 | 云南养瑞科技集团有限公司 | A kind of distillation apparatus of dynamic circulation extraction fragrance |
-
2017
- 2017-02-24 CN CN201720171672.8U patent/CN207031347U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106635082A (en) * | 2017-02-24 | 2017-05-10 | 山东腾鲁环保设备有限公司 | High-temperature dry distillation system |
| CN108485815A (en) * | 2018-05-29 | 2018-09-04 | 云南养瑞科技集团有限公司 | A kind of distillation apparatus of dynamic circulation extraction fragrance |
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